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1. 发明申请

WO2016199791A1 リアクタ审中-公开
标题翻译：反应堆
公开(公告)号：WO2016199791A1
公开(公告)日：2016-12-15
申请号：PCT/JP2016/066993
申请日：2016-06-08
申请人：株式会社IHI
发明人：矢野　明久 , 岡　辰哉 , 鎌田　博之 , 坂倉　茂樹 , 本間　信之 , 武内　佑介
IPC分类号： B01J19/24 , C01B3/38 , F28D9/00 , F28F3/00
CPC分类号： B01J12/007 , B01J19/0013 , B01J19/24 , B01J19/245 , B01J19/2485 , B01J2219/2414 , C01B3/38 , C01B3/384 , C01B3/48 , C01B2203/0233 , C01B2203/0238 , C01B2203/0283 , C01B2203/0833 , C01B2203/0883 , C01B2203/1241 , C07C1/041 , F28D9/00 , F28D9/0037 , F28D9/0093 , F28D2021/0022 , F28F3/00 , F28F3/048
摘要：このリアクタは、原料流体と熱媒体との間の熱交換によって、原料流体を反応させて、生成物を生成するものであり、原料流体を流通させるメイン反応流路と、メイン反応流路内の原料流体の流れ方向に沿って熱媒体を流通させるメイン温調流路とを有するメインリアクタコアと、出口側がメイン反応流路の入口側に連通しかつ原料流体を流通させるプレ反応流路と、入口側がメイン反応流路の出口側に連通しかつプレ反応流路内の原料流体の流れ方向に沿って熱媒体としての生成物を流通させるプレ温調流路とを有するプレリアクタコアとを具備する。
摘要翻译：该反应器通过原料流体和加热介质之间的热交换使原料流体反应而生成产物。反应器设有主反应堆堆芯和预反应堆芯。主反应堆堆芯具有：使原料流体流过的主反应流路; 以及使原料流体在主反应流路内流动的方向使加热介质流过的主温度控制流路。预反应堆芯具有：预反应流路，其出口侧与主反应流路的入口侧连通，使原料流体通过该流路流动; 以及预热控制流路，其入口侧与主反应流路的出口侧连通，使作为加热介质的产品沿着原料的方向流动流体在预反应流动路径内流动。

2. 发明申请

WO2016113812A1 燃料改質装置审中-公开
标题翻译：燃料改造
公开(公告)号：WO2016113812A1
公开(公告)日：2016-07-21
申请号：PCT/JP2015/006356
申请日：2015-12-21
申请人：株式会社デンソー
发明人：青柳　賢司 , 中川　陽介
IPC分类号： C01B3/38 , B01D53/86 , F02D19/08 , F02M27/02
CPC分类号： B01D53/94 , B01J10/007 , B01J2219/0022 , C01B3/38 , C01B3/384 , C01B2203/0233 , C01B2203/0811 , C01B2203/0833 , C01B2203/148 , C01B2203/1619 , C01B2203/84 , F02D19/0671 , F02D19/08 , F02M26/23 , F02M26/36 , F02M27/02 , F02M31/16 , Y02T10/126
摘要：　燃料と水とを改質触媒（１１１）上で水蒸気改質反応させる燃料改質装置（１００）は、燃料を噴射して改質触媒（１１１）に供給する燃料噴射部（１１２）と、改質触媒（１１１）の温度を測定する温度測定部（１１３，１２１）と、改質触媒（１１１）の再生処理が必要かどうかを判定する判定部（１２２）と、を備える。判定部（１２２）による判定は、水蒸気改質反応が生じている際における改質触媒（１１１）の温度変化に基づいて行われる。
摘要翻译：该燃料重整器（100）在重整催化剂（111）上导致燃料与水之间的蒸汽重整反应，并且设置有用于向重整催化剂（111）供给喷射燃料的燃料喷射单元（112）测量重整催化剂（111）的温度的温度测量单元（113,121），以及确定是否需要重整催化剂（111）的再生处理的确定单元（122）。当进行蒸汽重整反应时，确定单元（122）基于重整催化剂（111）中的温度变化进行测定。

3. 发明申请

WO2014093335A1 COPRODUCTION OF OXYGEN, HYDROGEN, AND NITROGEN USING ION TRANSPORT MEMBRANES 审中-公开
标题翻译：使用离子交换膜对氧，氢和氮的共同作用
公开(公告)号：WO2014093335A1
公开(公告)日：2014-06-19
申请号：PCT/US2013/074114
申请日：2013-12-10
申请人： L'AIR LIQUIDE, SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DES PROCEDES GEORGES CLAUDE , GROVER, Bhadra, S.
发明人： GROVER, Bhadra, S.
IPC分类号： C01B13/02 , C01B21/04 , C01B3/38 , B01J19/24
CPC分类号： C01B13/0251 , B01J19/2475 , C01B3/382 , C01B3/384 , C01B21/0438 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0833 , C01B2203/0844 , C01B2203/1258
摘要： A method for the coproduction of oxygen, hydrogen and nitrogen using an ion transport membrane is provided. This method includes separating a compressed, hot air stream in an ion transport membrane, thereby producing a product oxygen stream and a hot nitrogen rich stream; utilizing at least a portion of the hot nitrogen rich stream as a heat source for reforming a hydrocarbons stream, thereby producing a syngas stream and a warm product nitrogen stream; and separating the syngas stream into a product hydrogen stream and a carbon dioxide rich stream.
摘要翻译：提供了使用离子迁移膜共生产氧，氢和氮的方法。该方法包括在离子迁移膜中分离压缩的热空气流，从而产生产物氧气流和富含热氮的气流; 利用富氮热流的至少一部分作为用于重整烃流的热源，从而产生合成气流和暖产物氮气流; 并将合成气流分离成产物氢气流和富二氧化碳流。

4. 发明申请

WO2014081627A1 METHOD FOR PRODUCING A GASEOUS FUEL COMPRISING HYDROGEN FROM KINETIC AND/OR POTENTIAL ENERGY RECOVERED FROM A VEHICLE POWERED BY A FOUR STROKE DIESEL ENGINE FITTED WITH AN ENGINE BRAKING MECHANISM AND SYSTEM USEFUL TO IMPLEMENT SUCH METHOD 审中-公开
标题翻译：生产包含氢的动力和/或潜在能量的气体燃料的方法，该动力学和/或潜在能量由配备发动机制动机构的四冲程柴油发动机所驱动的动力和用于实施该方法的系统
公开(公告)号：WO2014081627A1
公开(公告)日：2014-05-30
申请号：PCT/US2013/070283
申请日：2013-11-15
申请人： WALDERSON MIAMI LLC
发明人： BASTOS, Carlos, Manuel
IPC分类号： C01B3/32
CPC分类号： F02B43/00 , B01J8/067 , B01J2208/00221 , B01J2219/00006 , C01B3/30 , C01B3/384 , C01B2203/0233 , C01B2203/0833 , F02M21/0227 , F02M25/12 , Y02T10/121 , Y02T10/16 , Y02T10/32
摘要： A method for producing a hydrogen gaseous fuel from kinetic and/or potential energy recovered from a vehicle powered by a four stroke Diesel engine fitted with a Jacobs engine brake during a deceleration stage. Such a method comprises the following stages: a) providing a preheated steam flow; b) providing a gas flow from at least one chemical species used as preheated carbon and hydrogen source; c) mixing the gas flow from at least one chemical species used as carbon and hydrogen source from stage a) with the steam flow from stage b).
摘要翻译：一种从在由减速阶段装配有雅可比发动机制动器的四冲程柴油发动机驱动的车辆中回收的动能和/或势能产生氢气体燃料的方法。这种方法包括以下阶段：a）提供预热的蒸汽流; b）提供来自用作预热碳和氢源的至少一种化学物质的气流; c）将来自阶段a）的用作碳和氢源的至少一种化学物质的气流与来自阶段b）的蒸汽流混合。

5. 发明申请

WO2014058907A1 INTEGRATED HYDROPROCESSING 审中-公开
标题翻译：综合水力发电
公开(公告)号：WO2014058907A1
公开(公告)日：2014-04-17
申请号：PCT/US2013/063923
申请日：2013-10-08
申请人： VENTECH ENGINEERS INTERNATIONAL LLC
发明人： ARMISTEAD, George , MAY, Simon , STANLEY, Bill
IPC分类号： C10G49/00 , C01B3/34 , C10L3/10 , C10G2/00
CPC分类号： C10G7/08 , B01J19/00 , C01B3/38 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/062 , C01B2203/0833 , C10G2/00 , C10G2/32 , C10G45/02 , C10G45/58 , C10G47/00 , C10G49/00 , C10G2300/1022 , C10G2300/1048 , C10L3/12
摘要： The present invention relates to a method and system for converting gas to liquids and fractionating crude oil or condensate. Advantageously, it includes hydroprocessing at least a portion of the fractionated product and at least a portion of the Fischer-Tropsch products in the same hydroprocessor. Among other advantages the present invention provides for improved output quality for diesel and/or naphtha, reduced transportation and/or storage costs, and/or enhanced energy efficiency.
摘要翻译：本发明涉及将气体转化为液体并分馏原油或冷凝物的方法和系统。有利地，它包括在相同的加氢处理器中加氢处理分馏产物的至少一部分和费 - 托产物的至少一部分。本发明还有其它优点提供改善柴油和/或石脑油的输出质量，减少运输和/或储存成本，和/或提高能量效率。

6. 发明申请

WO2013188671A2 STEAM REFORMERS, MODULES, AND METHODS OF USE 审中-公开
标题翻译：蒸汽改性剂，模块和使用方法
公开(公告)号：WO2013188671A2
公开(公告)日：2013-12-19
申请号：PCT/US2013/045665
申请日：2013-06-13
申请人： NUVERA FUEL CELLS, INC.
发明人： ZHAO, Jian, L. , KIM, Changsik , SHI, Yanlong
IPC分类号： C01B3/38 , B01J8/06
CPC分类号： B01J7/02 , B01J8/062 , B01J8/067 , B01J2208/00203 , B01J2208/00221 , B01J2208/00407 , B01J2208/00415 , B01J2208/00495 , B01J2208/00504 , B01J2208/0053 , C01B3/26 , C01B3/384 , C01B2203/0233 , C01B2203/0805 , C01B2203/0811 , C01B2203/0833 , C01B2203/1614 , Y02P20/134
摘要： The present disclosure is directed to steam reformers for the production of a hydrogen rich reformate, comprising a shell having a first end, a second end, and a passage extending generally between the first end and the second end of the shell, and at least one heat source disposed about the second end of the shell. The shell comprises at least one conduit member comprising at least one thermally emissive and high radiant emissivity material, at least partially disposed within the shell cavity. The shell further comprises at least one reactor module at least a portion of which is disposed within the shell cavity and about the at least one conduit member and comprises at least one reforming catalyst. The disclosure is also directed to methods of producing a hydrogen reformate utilizing the steam reformers, comprising the steps of combusting a combustible mixture in a burner to produce a combustion exhaust that interacts with the steam reactor module(s) through surface to surface radiation and convection heat transfer, and reforming a hydrocarbon fuel mixed with steam in the steam reformers to produce a hydrogen-containing reformate. The present disclosure is further directed to reactor modules for use with the above steam reformers and methods of producing a hydrogen reformate.
摘要翻译：本公开涉及用于生产富氢重整油的蒸汽重整器，其包括壳体，壳体具有第一端部，第二端部和大体上在壳体的第一端部和第二端部之间延伸的通道，以及至少一个围绕壳的第二端设置的热源。壳体包括至少一个导管构件，其包括至少部分地设置在壳腔内的至少一个热发射和高辐射辐射材料。壳体还包括至少一个反应器模块，其至少一部分设置在壳体腔内并且围绕至少一个管道构件并且包括至少一个重整催化剂。本公开还涉及使用蒸汽重整器生产氢转化率的方法，包括以下步骤：在燃烧器中燃烧可燃混合物以产生与蒸汽反应器模块相互作用的燃烧排放物，所述燃烧废气通过表面对辐射和对流在蒸汽重整器中与蒸汽混合的烃燃料进行热传递和重整以产生含氢重整产物。本公开进一步涉及与上述蒸汽重整器一起使用的反应器模块以及生产重整氢气的方法。

7. 发明申请

WO2013137720A1 METHOD AND SYSTEM FOR THE PRODUCTION OF HYDROGEN 审中-公开
标题翻译：用于生产氢的方法和系统
公开(公告)号：WO2013137720A1
公开(公告)日：2013-09-19
申请号：PCT/NL2013/050157
申请日：2013-03-11
申请人： STAMICARBON B.V. ACTING UNDER THE NAME OF MT INNOVATION CENTER
发明人： MORICO, Barbara , SALLADINI, Annarita , IAQUANIELLO, Gaetano
IPC分类号： C01B3/38 , B01J8/00 , B01J8/06 , C01B3/48
CPC分类号： C01B3/382 , B01J7/00 , B01J8/009 , B01J8/067 , B01J19/02 , B01J2208/00212 , B01J2219/0004 , B01J2219/0286 , C01B3/384 , C01B3/48 , C01B3/501 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/0833 , C01B2203/143 , C01B2203/146 , C01B2203/82 , Y02P20/134
摘要： Disclosed is a process for the production of hydrogen in a reactor system comprising a steam reforming reaction zone comprising a reforming catalyst and a membrane separation zone comprising a hydrogen-selective membrane. The process involves a reaction system of so-called open architecture, wherein the reforming zone and the membrane separation zone operate independently of each other. The invention provides the heat for the reforming reaction through heat exchange from liquid molten salts, preferably heated by solar energy.
摘要翻译：公开了一种在反应器系统中生产氢气的方法，其包括包含重整催化剂和包含氢选择性膜的膜分离区的蒸汽重整反应区。该方法涉及所谓的开放结构的反应体系，其中重整区和膜分离区彼此独立地操作。本发明通过液体熔融盐的热交换提供热重整反应，优选由太阳能加热。

8. 发明申请

WO2013033711A1 INTEGRATION OF FT SYSTEM AND SYN-GAS GENERATION 审中-公开
标题翻译： FT系统和SYN-GAS生成的整合
公开(公告)号：WO2013033711A1
公开(公告)日：2013-03-07
申请号：PCT/US2012/053685
申请日：2012-09-04
申请人： GTLPETROL LLC , ALLAM, Rodney J.
发明人： ALLAM, Rodney J.
IPC分类号： C01B3/24 , C10G1/00 , B01D15/30 , B01J19/00
CPC分类号： B01D3/34 , B01D53/1406 , B01D53/1475 , B01D53/1487 , B01D2252/205 , B01D2257/702 , C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/043 , C01B2203/0495 , C01B2203/062 , C01B2203/0833 , C01B2203/0894 , C01B2203/1258 , C01B2203/141 , C01B2203/148 , C10G2300/1022 , C10K1/143 , Y02P20/152
摘要： In some implementations, a method for separating components includes receiving off-gas from a Fischer-Tropsch hydrocarbon synthesis reaction process. The off-gas is scrubbed with a light oil at least proximate atmospheric temperature to substantially remove a mixture of C 3 and C 4 . The C 3 and C 4 are separated from the mixture into two separate streams using distillation columns in a Fischer-Tropsch system.
摘要翻译：在一些实施方案中，用于分离组分的方法包括从费 - 托烃合成反应过程接收废气。废气用至少接近大气温度的轻油擦洗，以基本上除去C3和C4的混合物。使用费 - 托系统中的蒸馏塔将C3和C4从混合物分离成两个分开的流。

9. 发明申请

WO2010104732A3 CONTROLLING THE SYNTHESIS GAS COMPOSITION OF A STEAM METHANE REFORMER 审中-公开
标题翻译：控制蒸汽甲烷改性剂的合成气组成
公开(公告)号：WO2010104732A3
公开(公告)日：2011-01-13
申请号：PCT/US2010026179
申请日：2010-03-04
申请人： UNIV CALIFORNIA , NORBECK JOSEPH M , PARK CHAN SEUNG , RAJU ARUN SK , KIM KISEOK
发明人： NORBECK JOSEPH M , PARK CHAN SEUNG , RAJU ARUN SK , KIM KISEOK
IPC分类号： C01B3/02 , C01B3/34 , C01B3/24 , C07C27/06 , C10G1/00 , C10G2/00 , C10J3/00 , C10J3/54 , C10J3/66 , G06F17/00
CPC分类号： C01B3/34 , C01B2203/00 , C01B2203/0233 , C01B2203/04 , C01B2203/0495 , C01B2203/06 , C01B2203/062 , C01B2203/0827 , C01B2203/0833 , C01B2203/0838 , C01B2203/0883 , C01B2203/0894 , C01B2203/1205 , C01B2203/1258 , C01B2203/1276 , C01B2203/146 , C01B2203/148 , C01B2203/1642 , C01B2203/84 , C10G1/002 , C10G2/30 , C10G2/32 , C10G2300/1003 , C10G2300/1011 , C10G2300/1014 , C10G2300/201 , C10J3/00 , C10J3/54 , C10J3/66 , C10J3/721 , C10J3/723 , C10J2300/06 , C10J2300/0903 , C10J2300/0906 , C10J2300/0916 , C10J2300/092 , C10J2300/093 , C10J2300/0946 , C10J2300/0966 , C10J2300/0973 , C10J2300/0983 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10J2300/1693 , C10J2300/1807 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/143 , C10K1/16 , C10K1/165 , C10K3/005 , C10K3/006 , Y02E20/18 , Y02E50/32 , Y02P20/128 , Y02P20/145 , Y02P30/20
摘要： An improved, economical alternative method to supply steam and methane to a steam methane reformer (SMR) is accomplished by a combination of procedures, wherein product gas from a steam hydro-gasification reactor (SHR) is used as the feedstock for the SMR by removing impurities from the product stream from the SHR with a combination of autothermai reforming, condensation removal and gas cleanup procedures that operates substantially at process pressures and at a temperature above the boiling point of water at the process pressure, is located between the SHR and SMR. In another embodiment, a method is provided for controlling the H2/CO syngas ratio obtained from a steam methane reformer (SMR) by adjusting the hydrogen feed and the water content of feedstock into a steam hydro-gasification reactor that supplies the SMR.
摘要翻译：向蒸汽甲烷重整器（SMR）提供蒸汽和甲烷的改进的，经济的替代方法是通过以下步骤完成的，其中将来自蒸汽加氢气化反应器（SHR）的产物气体用作SMR的原料，通过除去来自SHR的产物流中的杂质具有自动干燥重整，冷凝去除和气体净化程序的组合，其基本上在过程压力下和在高于过程压力的沸点的温度下操作，位于SHR和SMR之间。在另一个实施方案中，提供了一种方法，用于通过将氢气进料和原料的水含量调节到供应SMR的蒸汽加氢气化反应器中来控制从蒸汽甲烷重整器（SMR）获得的H 2 / CO合成气比。

10. 发明申请

WO2010104732A2 CONTROLLING THE SYNTHESIS GAS COMPOSITION OF A STEAM METHANE REFORMER 审中-公开
标题翻译：控制蒸汽甲烷改性剂的合成气组成
公开(公告)号：WO2010104732A2
公开(公告)日：2010-09-16
申请号：PCT/US2010/026179
申请日：2010-03-04
申请人： THE REGENTS OF THE UNIVERSITY OF CALIFORNIA , NORBECK, Joseph, M. , PARK, Chan, Seung , RAJU, Arun, Sk , KIM, Kiseok
发明人： NORBECK, Joseph, M. , PARK, Chan, Seung , RAJU, Arun, Sk , KIM, Kiseok
IPC分类号： C01B3/34 , C01B3/24 , C10J3/00 , G06F17/00
CPC分类号： C01B3/34 , C01B2203/00 , C01B2203/0233 , C01B2203/04 , C01B2203/0495 , C01B2203/06 , C01B2203/062 , C01B2203/0827 , C01B2203/0833 , C01B2203/0838 , C01B2203/0883 , C01B2203/0894 , C01B2203/1205 , C01B2203/1258 , C01B2203/1276 , C01B2203/146 , C01B2203/148 , C01B2203/1642 , C01B2203/84 , C10G1/002 , C10G2/30 , C10G2/32 , C10G2300/1003 , C10G2300/1011 , C10G2300/1014 , C10G2300/201 , C10J3/00 , C10J3/54 , C10J3/66 , C10J3/721 , C10J3/723 , C10J2300/06 , C10J2300/0903 , C10J2300/0906 , C10J2300/0916 , C10J2300/092 , C10J2300/093 , C10J2300/0946 , C10J2300/0966 , C10J2300/0973 , C10J2300/0983 , C10J2300/165 , C10J2300/1659 , C10J2300/1671 , C10J2300/1675 , C10J2300/1693 , C10J2300/1807 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/143 , C10K1/16 , C10K1/165 , C10K3/005 , C10K3/006 , Y02E20/18 , Y02E50/32 , Y02P20/128 , Y02P20/145 , Y02P30/20
摘要： An improved, economical alternative method to supply steam and methane to a steam methane reformer (SMR) is accomplished by a combination of procedures, wherein product gas from a steam hydro-gasification reactor (SHR) is used as the feedstock for the SMR by removing impurities from the product stream from the SHR with a combination of autothermai reforming, condensation removal and gas cleanup procedures that operates substantially at process pressures and at a temperature above the boiling point of water at the process pressure, is located between the SHR and SMR. In another embodiment, a method is provided for controlling the H2/CO syngas ratio obtained from a steam methane reformer (SMR) by adjusting the hydrogen feed and the water content of feedstock into a steam hydro-gasification reactor that supplies the SMR.
摘要翻译：向蒸汽甲烷重整器（SMR）提供蒸汽和甲烷的改进的，经济的替代方法是通过以下步骤完成的，其中将来自蒸汽加氢气化反应器（SHR）的产物气体用作SMR的原料，通过除去来自SHR的产物流中的杂质具有自动干燥重整，冷凝去除和气体净化程序的组合，其基本上在过程压力下和在高于过程压力的沸点的温度下操作，位于SHR和SMR之间。在另一个实施方案中，提供了一种方法，用于通过将氢气进料和原料的水含量调节到供应SMR的蒸汽加氢气化反应器中来控制从蒸汽甲烷重整器（SMR）获得的H 2 / CO合成气比。

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